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Binderless zeolite adsorbent and preparation method thereof

A technology without binder and adsorbent, applied in chemical instruments and methods, inorganic chemistry, other chemical processes, etc., can solve the problems of low adsorption rate, small adsorption capacity, and high adsorption rate

Active Publication Date: 2014-11-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] One of the technical problems to be solved by the present invention is that the existing binderless adsorbents have the problems of small adsorption capacity and low adsorption rate due to the use of clay binders, and a new binderless A Type zeolite adsorbent, which has the advantages of large adsorption capacity and high adsorption rate

Method used

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  • Binderless zeolite adsorbent and preparation method thereof
  • Binderless zeolite adsorbent and preparation method thereof
  • Binderless zeolite adsorbent and preparation method thereof

Examples

Experimental program
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Embodiment 1

[0018] Take by weighing sodium aluminate (by weight percentage, containing Al 2 o 3 41%) 200 grams, in a 3000 milliliter beaker, add 1000 milliliters of water and stir to dissolve, add a certain amount of sodium hydroxide or sulfuric acid, keep Na 2 O / SiO 2 =0.75~1.6, then add 250 grams of silica sol (40 wt%), transfer to a 4000 ml reaction kettle, and crystallize at 70° C. for 10 hours. The product was taken out, washed with deionized water until neutral, and dried at 120°C for 10 hours to obtain 4A molecular sieve. The molecular sieve is mixed with sodium silicate with a weight ratio of 10%, and rolled into a ball to form the shaped adsorbent of the present invention. Shaped adsorbent and Al containing by weight percent 2 o 3 Mix with 15% alkaline sodium aluminate aqueous solution, so that the total molar ratio in the mixed system is Si / Al=1.0~2.5, Na 2 O / SiO 2 =0.50~1.6, soaked for 6 hours, moved into an airtight container, heated and crystallized step by step, after...

Embodiment 2~9

[0022] The preparation method of Examples 2-9 is exactly the same as that of Example 1, except that the ratio of raw materials, the type of binder, the amount of Al in the alkaline aqueous solution 2 o 3 The concentration and the specific crystallization conditions are different. The ratio of raw materials for the synthesis of molecular sieves is shown in Table 1, the type and amount of binder and Al in alkaline aqueous solution 2 o 3 The concentration is shown in Table 2, and the step-by-step crystallization conditions are shown in Table 3. After the adsorbent was dried, it was activated at 350°C for 2 hours, and then cooled to room temperature in a desiccator to evaluate the adsorption performance of the adsorbent. The evaluation conditions of the adsorbent are exactly the same as in Example 1, and the performance and evaluation results of the adsorbent are shown in Table 4.

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Abstract

The present invention relates to a binderless zeolite adsorbent and a preparation method thereof, and is mainly to solve the problem of small adsorbent capacity, low adsorption rate, and high impurity content in the adsorbent in the prior art. A technical solution solves the technical problems well. According to the present invention, the binderless zeolite adsorbent has particle size of 16-40 meshes, and strength >= 60 N / particle. At room temperature and the solid-liquid ratio of 3:5, the adsorption capacity of the binderless zeolite adsorbent for n-hexane in a cyclohexane solution containing 10% of n-hexane by weight is greater than 0.11 g per gram of the adsorbent, and the adsorption rate is greater than 16 mg / gram of the adsorbent / minute in initial 5 minutes. The binderless zeolite adsorbent can be used for adsorption and separation of n-alkanes in naphtha.

Description

technical field [0001] The invention relates to a binderless zeolite adsorbent and a preparation method thereof. Background technique [0002] Naphtha is composed of a mixture of various hydrocarbons such as n-alkanes, isoparaffins, naphthenes and aromatics. For steam cracking ethylene, different types of hydrocarbons contribute differently to ethylene formation. The ethylene yield of normal alkanes is the highest, followed by naphthenes and isoparaffins, while aromatics do not contribute to ethylene formation. On the other hand, as a raw material for catalytic reforming, the reaction rate of cyclodehydrogenation of normal alkanes to aromatics is very slow and the conversion rate is low. Therefore, using molecular sieve adsorbent to separate n-alkanes in naphtha is an effective method to make full use of naphtha. [0003] The most effective adsorbent for separating n-alkanes is 5A molecular sieve. Its average pore diameter is The molecular diameter of normal alkanes is...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J20/18B01J20/28B01J20/30
Inventor 孔德金钱斌郑钧林陈燕杨德琴
Owner CHINA PETROLEUM & CHEM CORP